Nghiên cứu này sử dụng dịch nha với ñộ chất khô 30oBx và ñược bổ sung thế liệu là
sirô maltose ñể thực hiện quá trình lên men bia nồng ñộ rất cao. Khi tăng tỉ lệ giống cấy từ 25 triệu lên
125 triệu tế bào/mL, thời gian lên men sẽ rút ngắn, hàm lượng ethanol và diacetyl trong bia non sẽ tăng
lên. Tỉ lệ giống cấy thích hợp là 75 triệu tế bào/mL. Khi ñó, thời gian lên men giảm 44.2%, nồng ñộ
ethanol trong bia non tăng 13.7% so với mẫu ñối chứng sử dụng tỉ lệ giống cấy theo phương pháp
truyền thống; hiệu suất sinh tổng hợp ethanol ñạt giá trị cực ñại là 44.1%. Khi kết hợp giải pháp sử
dụng tỉ lệ giống cấy cao với giải pháp bổ sung chất dinh dưỡng vào dịch nha 30oBx thì thời gian lên
men sẽ giảm 8.7% so với trường hợp chỉ sử dụng tỉ lệ giống cấy cao, còn nồng ñộ ethanol trong bia non
và hiệu suất sinh tổng hợp ethanol thu ñược sẽ không thay ñổi.
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TAÏP CHÍ PHAÙT TRIEÅN KH&CN, TAÄP 14, SOÁ K4 - 2011
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EFFECTS OF HIGH PITCHING RATE AND NUTRITIONAL SUPPLEMENTION
ON YEAST FERMENTATION PERFORMANCE IN VERY HIGH GRAVITY
BREWING
Vo Dang Minh Nguyet, Le Van Viet Man
University of Technology, VNU-HCM
(Manuscript Received on December 16th, 2010, Manuscript Revised June 06th, 2011)
ABSTRACT: In this study, the 30oBx wort with 30% maltose syrup adjunct was used for very
high gravity brewing. Increase in pitching rate from 25×106 cells/mL to 125×106 cells/mL shortened the
primary fermentation time and augmented the level of ethanol and diacetyl in the green beer. The
suitable pitching rate was 75×106 cells/mL. Under this condition, the fermentation time reduced 44.2%
and the ethanol concentration in the green beer increased 13.7% in comparison with those in the
culture with conventional pitching rate; the ethanol yield achieved maximum of 44.1%. Combination of
high pitching rate and nutritional supplementation to 30oBx wort reduced the fermentation time 8.7%
and maintained the similar ethanol content in the green beer and the similar ethanol yield in
comparison with the high pitching rate culture.
Keywords: pitching rate, Tween 80, very high gravity brewing, yeast extract.
1. INTRODUCTION
The high-gravity brewing technology has
become widespread throughout the brewing
industry during the past 35 years. This method
of beer production has many advantages such
as: increased brewery capacity by 20–30%
without additional expenditures for facilities,
reduced cost of energy and labor [1], improved
physical and flavor stability of beer, more
alcohol per unit of fermentable extract due to
reduced yeast growth, higher adjunct rates [2].
High-gravity brewing also offers a flexibility of
the beer type (products with different sugar or
alcohol levels) [1]. Many researches were
carried out to increase wort gravity in high
gravity brewing [3,4]. However, the obtained
results showed that the yeast viability was
rapidly reduced within 24 hours after pitching,
the fermentation rates decreased and the
ethanol yield was lower when the wort gravity
was more than 24°P [3]. In high gravity wort,
the yeasts are exposed to severe conditions
such as high osmotic pressure and toxicity of
produced ethanol [1], nutrient limitation such
as assimilable nitrogen and fatty acids [4].
These arising problems have been solved
with high pitching rates [5], nutrient
supplementation to wort [4], more efficient
aeration than in conventional brewing [6]
Among those solutions, high pitching rates are
advantageous in many respects [5]. Attenuation
begins more rapidly, and viability losses that
occur immediately after pitching are not
apparent. Moreover, the profiles of volatile
flavor in the beer produced were relatively
unaffected by increased inoculum size [4].
Science & Technology Development, Vol 14, No.K4- 2011
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There have been various studies on the
effects of pitching levels on beer fermentation,
the wort gravity varied from 15 to 24oP [2,7].
This study focused on the effects of pitching
rate on yeast fermentation performance in very
high gravity wort (30oBx). In addition,
combined application of high pitching rate and
nutritional supplementation to 30oBx wort was
also examined.
2. MATERIALS AND METHODS
2.1. Materials
Wort: 30oBx wort was prepared by adding
high maltose syrup to an all-malt wort and the
ratio of high maltose syrup adjunct was 30%.
High maltose syrup (80% dissolved solids, 42
dextrose equivalent) was supplied by Bien Hoa
Confectionery Joint Stock Company. All–malt
wort was produced from barley malt by
infusion mashing. Barley malt (extraction
yield: 79.2%) was originated from Australia
and supplied by Duong Malt Co., Ltd.
Chemicals: In some experiments, yeast
extract (Merck and Co., Inc) and Tween 80
(0.6% free oleic acid) (Shantou Xilong
Chemical Factory, Guangdong) were added to
high gravity wort as sources of assimilable
nitrogen and unsaturated fatty acid.
Yeast: Lager brewing strain of
Saccharomyces cerevisiae used in this study
was originated from Microorganism collection
of Food Microbiology Laboratory, Department
of Food Technology, Ho Chi Minh City
University of Technology. Yeast propagation
was performed in the 16oBx all – malt wort in
an incubator at 30oC. The required inoculum
size was prepared by centrifuging the culture
above at 6000 rpm at 4°C for 15 min.
2.2. Fermentation
Fermentation was carried out in a
bioreactor containing 2L of sterile 30oBx wort.
Initial content of dissolved oxygen (prior to
inoculation) was 8 ppm. The primary
fermentation was conducted at 17oC and
completed when 80% of the reducing sugars
had been consumed.
Effects of high pitching rate on yeast
fermentation performance
In this experiment, five pitching rates
(25×106, 50×106, 75×106, 100×106 and
125×106 cells/mL) were used.
Combined high pitching rate and
nutritional supplementation to wort in very
high gravity brewing: Optimization of
supplemented nutrients for yeast by response
surface methodology
Assimilable nitrogen (yeast extract) and
unsaturated fatty acid (Tween 80) were added
to the 30oBx wort as supplemented nutrients for
brewing yeast. The experiment was carried out
according to a randomised, quadratic central
composite circumscribed response surface
design with 2 independent variables and 5
levels. Two variables included yeast extract
level (X1) and Tween 80 level (X2). Ethanol
concentration in the green beer (Y) was the
dependent variable. The experimental design is
shown in Table 2. The complete design
consisted of 12 experimental points including 4
factorial points, 4 axial points and 4 center
TAÏP CHÍ PHAÙT TRIEÅN KH&CN, TAÄP 14, SOÁ K4 - 2011
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points and the experiment was carried out in a
random order. The software Modde version 5.0
was used to generate the experimental planning
and to process data. The pitching rate was fixed
at 75×106 cells/mL.
2.3. Fermentation analysis
Samples were daily removed in order to
determine total yeast cell number, yeast
viability, reducing sugar, ethanol, and diacetyl
concentration. Yeast cell number was
quantified by using Thoma Haemocytometry.
Viable cells were determined by using
methylene blue staining [8]. Reducing sugars
were quantified by spectrophotometric method
using dinitrosalicylic acid reagent [9]. Free
amino nitrogen (FAN) content was measured
by spectrophotometric method, using ninhydrin
reagent [8]. Ethanol concentration was
determined by a method based on distillation
and density quantification [9]. Diacetyl was
determined by spectrophotometric method
using O–phenylendiamin reagent [8].
Maximum specific growth rate was
calculated by a method reported elsewhere
[10]. The sugar uptake rate (g/L.h) was
calculated as the ratio of the reducing sugar
content (g/L) assimilated by yeast to the
fermentation time (h). The ethanol production
rate (g/L.h) was calculated as the ratio of the
ethanol content produced by yeast to the
fermentation time (h).
2.4. Statistical analysis
All fermentations were realized in
duplicated. The data was analyzed for
statistical significance by Analysis of Variance
using the soflware Statgraphics plus version
3.2.
3. RESULTS AND DISCUSSION
3.1. Effect of pitching rate on yeast
fermentation performance
Fermentation performance
Fig. 1 shows the kinetics of sugar
assimilation. The concentration of reducing
sugars in the cultures with high pitching rates
decreased significantly faster than that in the
culture with conventional pitching rate (25×106
cells/mL). Table 1 demonstrates that the sugar
uptake rate in the cultures with pitching rate of
50×106, 75×106, 100×106 and 125×106
cells/mL increased 35.8%, 78.8%, 92.7% and
122.6%, respectively, in comparison with that
in the control. This observation was in
agreement with the results of Erten (2007) who
examined the effect of inoculum size on sugar
uptake rate on the 16oP wort [2].
Science & Technology Development, Vol 14, No.K4- 2011
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Fig 1. Sugar assimilation during the fermentation
() 25106 cells/mL, () 50106 cells/mL, () 75 106 cells/mL, () 100106 cells/mL, () 125106
cells/mL
The higher the pitching rate, the higher the
sugar uptake rates and the shorter the
fermentation time. The time required to reach a
fermentation degree of 80% was approximately
163 hours for the conventional inoculum size
(25×106 cells/mL), 120h for two-fold higher
pitching rate, 91h for the three-fold higher
pitching rate, 85h for the four-fold higher
pitching rate and 74 h for the highest pitching
rate (125×106 cells/mL). Noteworthy, when the
pitching rate increased from 25×106 to 75×106
cells/mL, a reduction of the fermentation time
of 60% was achieved (Table 1).
Similarly, the ethanol production rate
increased 53.1%, 103.8%, 118% and 154%
when the pitching rate augmented two-, three-,
four- and five-fold, respectively higher than the
conventional value. A slightly increase in
ethanol concentration in the green beer was
also observed in the culture with increased
inoculum size.
The ethanol yield was improved when the
pitching rate increased from 25×106 to 75×106
cells/mL. At higher pitching rates, the analysis
of variance showed that the ethanol yield
decreased slightly. The highest ethanol yield
reached 44.1% in the culture with the pitching
rate of 75×106 cells/mL. According to Suihko
et al. 1993, as the original wort gravity
increased, more fermentable extract was
metabolized to ethanol rather than utilized for
yeast growth [11].
Yeast growth
Fig. 2 illustrates the kinetics of yeast
growth in the cultures with different pitching
rates. Increase in pitching rate augmented the
maximum cell number in the culture. The
results show that maximum cell number in the
culture with the highest pitching rate (125×106
cells/mL) was 68.3% higher than that in the
culture with the conventional pitching rate.
However, the net growth in the cultures with
TAÏP CHÍ PHAÙT TRIEÅN KH&CN, TAÄP 14, SOÁ K4 - 2011
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high pitching rate (50×106, 75×106, 100×106
and 125×106 cells/mL) was not significantly
different from that in the culture with
conventional pitching rate. Hence, the same
amount of new yeast cells was generated
during the fermentation in all examined
cultures. This means that at the end of
fermentation, the yeast population in the
cultures with high pitching rate had a higher
percentage of ‘older’ cells. Our result was also
in agreement with the findings of Verbelen et
al. (2008) who carried out high gravity brewing
with 15oP all-malt wort [7].
0
50
100
150
200
250
0 24 48 72 96 120 144 168
Ye
as
t c
o
n
ce
n
tr
at
io
n
(10
6
ce
lls
/m
L)
Fermentation time (hours)
Fig 2. Kinetics of yeast growth during the fermentation.
() 25106 cells/mL, () 50106 cells/mL, () 75 106 cells/mL, () 100106 cells/mL, () 125106
cells/mL
Table 1 also presents that the maximum
specific growth rate of yeast at the
conventional pitching rate was the highest
(0.065h-1). When the pitching rate increased
two-, three-, four- and five-fold higher than the
conventional value, the maximum specific
growth rate decreased 52.3%, 64.6%, 63.1%
and 72.3%, respectively. At the beginning of
the fermentation, the yeast viability was
approximately 98%. The percentage of viable
cells at the end of the fermentation remained
above 86% in the four cultures with high
pitching rate. In the control, the percentage of
viable cells only reached 71% (Table 1).
Diacetyl content in the green beer
Diacetyl can cause a ‘buttery’ off-flavour
above its threshold of 80 ppb. Diacetyl is
formed by extracellular oxidative
decarboxylation of alpha acetolactate - an
intermediate in the biosynthesis pathway of
valine from pyruvate. Subsequently, yeast cells
assimilate and reduce diacetyl to the flavor
inactive compounds such as acetoin and 2, 3-
butanediol [12].
Science & Technology Development, Vol 14, No.K4- 2011
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Diacetyl in the green beer was present in
dramatically higher amounts with high pitching
rate particularly when the inoculum size was
100×106 cells/mL or higher (Table 1). This was
probably due to higher production alpha
acetolactate. Moreover, the shorter
fermentation time likely resulted in incomplete
reduction of diacetyl to acetoin and 2,3-
butanediol [12].
Table 1. Effect of five different pitching rates on fermentation characteristics in high gravity brewing
Pitching rate (x 106 cells/mL)
25 50 75 100 125
Fermentation time (hours)
Cell viability after fermentation (%)
Maximum specific growth rate (h-1)
Sugar uptake rate (g/L.h)
Ethanol production rate (g/L.h)
Ethanol concentration in the green beer (% v/v)
Ethanol production yield (%)
Diacetyl concentration in the green beer (mg/L) after
being diluted to ethanol concentration of 5% (v/v)
163a
71a
0.065a
1.37a
0.53a
10.98a
38.6a
0.31a
120b
86b
0.031b
1.86b
0.81b
12.36b
43.5b
0.53b
91c
97c
0.023c
2.45c
1.08c
12.48c
44.1b
0.59b
85d
94d
0.024c
2.64d
1.15d
12.45c
43.7b
0.81c
74e
97.5c
0.018d
3.05e
1.34e
12.64d
43.9b
0.97d
Different letters in each row mean significant difference (P< 0.05)
In summary, increase in inoculum size
shortened the fermentation time and increased
the level of ethanol and diacetyl in the green
beer. For 30oBx wort, the appropriate pitching
rate was 75×106 cells/mL, which allows both a
significant reduction of fermentation time and
an enhancement in ethanol concentration in the
green beer. As a result, 75×106 cells/mL was
chosen for the next experiment.
3.2. Combined high pitching rate and
nutritional supplementation to wort in very-
high gravity brewing: optimization of
supplemented nutrients for yeast by
response surface methodology
Based on the previous results of Dragone
et al. (2003) [13] and Casey et al. (1984) [4],
yeast extract level of 0.8% w/v and Tween 80
level of 0.24% v/v were chosen as the central
conditions of the central composite rotary
design. Table 3 show the ethanol concentration
in the green beer for each run obtained from the
experimentation.
TAÏP CHÍ PHAÙT TRIEÅN KH&CN, TAÄP 14, SOÁ K4 - 2011
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Table 2. Independent variables and their levels in the response surface design
Independent variables Symbol
Range and levels
- 21/2 -1 0 +1 +21/2
Yeast extract concentration % (w/v) X1 0.52 0.6 0.8 1.0 1.08
Tween 80 concentration % (v/v) X2 0.16 0.18 0.24 0.3 0.32
Table 3. Optimization of nutrient supplementation for yeast: experimental design and results
Exp.No. X1 X2 Response, Y% (v/v)
1 -1 -1 12.42
2 +1 -1 12.40
3 -1 +1 12.54
4 +1 +1 12.50
5 -21/2 0 12.48
6 +21/2 0 12.43
7 0 -21/2 12.38
8 0 +21/2 12.52
9 0 0 12.58
10 0 0 12.60
11 0 0 12.59
12 0 0 12.61
X1: yeast extract concentration, X2: Tween 80 concentration, Y: ethanol concentration in the green beer
In order to establish the fitted model,
multiple regression analysis was performed on
the experimental data and the final predictive
equation obtained is as given below:
Y= 12.60 – 0.02 X1 + 0.05 X2 – 0.06 X12 – 0.07 X22 (1)
where Y, X1 and X2 were the ethanol
concentration in the green beer (% v/v), the
yeast extract concentration (% w/v) and the
Tween 80 concentration (% v/v), respectively.
Table 4 presents ANOVA of the fitted
model. According to the ANOVA table, the
regression model is significant at the
considered confidence level (P < 0.05) since a
satisfactory correlation coefficient was
obtained and the F-value was higher than the F
listed value.
The effect of each variable on the response
is presented in Table 5 for a 95% confidence
level. The Tween 80 level had a stronger effect
on ethanol concentration than the yeast extract
level in the medium. Besides, no interaction
between the two variables on the ethanol
concentration was observed.
Fig. 3 presents the three-dimensional
response surface plot according to Eq. 1. From
the model, the optimal conditions were the
yeast extract concentration of 0.77% w/v and
the Tween 80 concentration of 0.26% v/v, at
Science & Technology Development, Vol 14, No.K4- 2011
Trang 12
which the model predicted a maximum
response of 12.61% v/v.
Finally, two cultures were realized and
compared: one culture with high pitching rate
(75×106 cells/mL) and one culture with high
pitching rate (75×106 cells/mL) and nutritional
addition (0.77% w/v yeast extract and 0.26%
v/v Tween 80 were supplemented to the 30oBx
wort).
Y% (v/v)
Fig 3. Response surface plot for maximizing ethanol concentration in the green beer Y% (v/v), X1: yeast extract
concentration % (w/v), X2: Tween 80 concentration % (v/v)
Table 4. Analysis of variance of the regression
model in experiments of supplemented nutrients
Source of
variation
DF SS MS F
Regression 5 1708.21 311.50 161.2
Residual 6 10.11 1.82
Total 11 1718.32 156.21
Listed F-
value*
6.4
SS: sum of squares, DF: degrees of freedom, MS:
mean square, F: F-value,* F-value at 95% of
confidence level.
Table 5. Estimated effect of independent variables
on ethanol concentration in the green beer
Factor* Effect Standard
error
P
X1 -0.020 0.0033 0.004035
X2 00520 0.0033 1.45E-005
X1 × X1 -0.060 0.0039 9.53E-006
X2 × X2 -0.070 0.0039 9.54E-006
X1: yeast extract concentration % (w/v), X2: Tween 80
concentration % (v/v), P indicates significance of linear
regressions. * Significant factor at 95% of confidence
level.
TAÏP CHÍ PHAÙT TRIEÅN KH&CN, TAÄP 14, SOÁ K4 - 2011
Trang 13
Table 6 shows that the combination of high
pitching rate and nutritional supplementation
shortened the fermentation time 8.7% in
comparison with the culture with high pitching
rate. In addition, the combined method
improved yeast viability (99%) at the end of
the fermentation. However, the ethanol
concentration in the green beer as well as the
ethanol yield in the two cultures were not
significantly different.
It can be affirmed that the combination of
high pitching rate and nutritional
supplementation to the very high gravity
brewing wort reduced notably the fermentation
time and still achieved high ethanol
concentration in the green beer and high
ethanol yield in very high gravity brewing.
Table 6. Fermentation characteristics of high gravity brewing
Sample with high
pitching rate
Sample with high
pitching rate and nutrient
addition*
Fermentation time (h) 92a 84b
Cell viability (%) 96a 99b
Ethanol concentration in the green beer (% v/v) 12.48a 12.61a
Ethanol production yield (%) 49.1a 49.6a
Diacetyl concentration in the green beer (mg/L)
after being diluted to ethanol concentration of
5% (v/v)
0.43a 0.51b
* 0.77% w/v yeast extract and 0.26% v/v Tween 80 was added to 30oBx wort prior to fermentation.
Different letters in each row mean significant difference (P< 0.05)
4. CONCLUSION
In 30oBx wort, increase in pitching rate
led to a faster fermentation rate as well as a
higher ethanol concentration in the green beer.
However, high pitching rate resulted in low
yeast growth and high diacetyl content in the
culture. The combination of high pitching rate
and nutritional addition to the wort reduced
fermentation time and increased the yeast
viability.
Science & Technology Development, Vol 14, No.K4- 2011
Trang 14
ẢNH HƯỞNG CỦA GIẢI PHÁP SỬ DỤNG TỈ LỆ GIỐNG CẤY CAO VÀ BỔ SUNG
CHẤT DINH DƯỠNG ðẾN HOẠT TÍNH LÊN MEN CỦA NẤM MEN
TRONG QUÁ TRÌNH LÊN MEN BIA NỒNG ðỘ RẤT CAO
Võ ðặng Minh Nguyệt, Lê Văn Việt Mẫn
Trường ðại học Bách khoa, ðHQG-HCM
TÓM TẮT: Nghiên cứu này sử dụng dịch nha với ñộ chất khô 30oBx và ñược bổ sung thế liệu là
sirô maltose ñể thực hiện quá trình lên men bia nồng ñộ rất cao. Khi tăng tỉ lệ giống cấy từ 25 triệu lên
125 triệu tế bào/mL, thời gian lên men sẽ rút ngắn, hàm lượng ethanol và diacetyl trong bia non sẽ tăng
lên. Tỉ lệ giống cấy thích hợp là 75 triệu tế bào/mL. Khi ñó, thời gian lên men giảm 44.2%, nồng ñộ
ethanol trong bia non tăng 13.7% so với mẫu ñối chứng sử dụng tỉ lệ giống cấy theo phương pháp
truyền thống; hiệu suất sinh tổng hợp ethanol ñạt giá trị cực ñại là 44.1%. Khi kết hợp giải pháp sử
dụng tỉ lệ giống cấy cao với giải pháp bổ sung chất dinh dưỡng vào dịch nha 30oBx thì thời gian lên
men sẽ giảm 8.7% so với trường hợp chỉ sử dụng tỉ lệ giống cấy cao, còn nồng ñộ ethanol trong bia non
và hiệu suất sinh tổng hợp ethanol thu ñược sẽ không thay ñổi.
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